EP0269583A2 - Méthode de préparation de résines de polyesters de haut poids moléculaire - Google Patents
Méthode de préparation de résines de polyesters de haut poids moléculaire Download PDFInfo
- Publication number
- EP0269583A2 EP0269583A2 EP87830402A EP87830402A EP0269583A2 EP 0269583 A2 EP0269583 A2 EP 0269583A2 EP 87830402 A EP87830402 A EP 87830402A EP 87830402 A EP87830402 A EP 87830402A EP 0269583 A2 EP0269583 A2 EP 0269583A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- granules
- carbon dioxide
- polycondensation
- treatment
- molecular weight
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
- C08G63/78—Preparation processes
- C08G63/80—Solid-state polycondensation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/0002—Condition, form or state of moulded material or of the material to be shaped monomers or prepolymers
Definitions
- This invention relates to a method for producing high molecular weight polyester resin, wherein granules of resin, in particular of polyethyleneterephtalate, are subjected to solid state polycondensation.
- High molecular weight polyester resins have been produced in the solid state at a lower temperature than the polymer melting temperature and either under a vacuum or an inert gas atmosphere.
- Such prior methods require, preparatory to polycondensation, partial or total crystallization of the granules under agitation, for example in either rotary units under vacuum or fluidized bed units, in order to prevent the granules from becoming stuck during polymerization. In fact, such sticking may turn the granules into a single lump, bringing the plant to a standstill.
- the granules of amorphous polymer in the methods disclosed in the above-mentioned patents need to be forcibly stirred at a first crystallization stage before the granules can be passed to a solid state polycondensation stage on a fixed bed.
- polyester granules must be stirred at a stage preceding the polycondensation stage is the cause for releasing large amounts of polymer dust and a high power consumption.
- the polymer dust as produced by fretting of the mechanical stirring devices against the granules and between granules, may create serious problems at the succeeding polycondensation stage, and the mechanical stirring devices are often a cause for stopping the plant either for servicing purposes or on account of malfunction of the stirrers, which are subjected to high mechanical stresses.
- the method comprises the step of treating the granules, prior to polycondensation, with carbon dioxide at a higher temperature than the critical temperature of carbon dioxide.
- the treatment is carried out with carbon dioxide in a supercritical condition.
- the amorphous polyester granules are effectively prevented from sticking to one another during the solid state polycondensation on a fixed bed.
- the granules of amorphous polyester are preferably subjected to an atmosphere containing carbon dioxide at a pressure in excess of 25 bars and at a lower temperature than the polymer melting temperature (approximately 240°C) for a sufficient time period to enable access to the polycondensation step without any risk of the granules becoming stuck together.
- This treatment time is normally in the range of 0.5 to 5 hours.
- a further advantage of the method according to the invention is that the amount of acetaldehyde present in the granules and the rate of acetaldehyde formation in the granules can be lowered. This significant side effects seemingly arise from that the carbon dioxide extracts the acetaldehyde from the granules and deactivates the catalysts in the granules themselves.
- the solid state polycondensation is carried out at a temperature within the range of 180°C to 240°C, preferably of 200°C to 230°C.
- Carbon dioxide, or another inert gas such as nitrogen, can be advantageously used at the polycondensation stage in a ratio of 0.4-3 kg/hour inert gas per kg/hour granules.
- the residence time of granules in the polycondensation stage was 20 hours.
- the CO2 coming out from the polycondensation stage was cycled back following purification of the volatile substances formed during the polycondensation.
- the PET granules yielded by the polycondensation stage had an acetaldehyde content of 0.4 ppm and an acetaldehyde generation rate at 270°C of 0.25 ppm acetaldehyde/minute.
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Polyesters Or Polycarbonates (AREA)
- Looms (AREA)
- Breeding Of Plants And Reproduction By Means Of Culturing (AREA)
- Radar Systems Or Details Thereof (AREA)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT87830402T ATE90953T1 (de) | 1986-11-21 | 1987-11-12 | Verfahren zur herstellung von hochmolekularen polyesterharzen. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IT22424/86A IT1199668B (it) | 1986-11-21 | 1986-11-21 | Procedimento per la produzione di resina poliestere ad alto peso molecolare |
IT2242486 | 1986-11-21 |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0269583A2 true EP0269583A2 (fr) | 1988-06-01 |
EP0269583A3 EP0269583A3 (en) | 1990-01-31 |
EP0269583B1 EP0269583B1 (fr) | 1993-06-23 |
Family
ID=11196125
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP87830402A Expired - Lifetime EP0269583B1 (fr) | 1986-11-21 | 1987-11-12 | Méthode de préparation de résines de polyesters de haut poids moléculaire |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP0269583B1 (fr) |
AT (2) | ATE90953T1 (fr) |
DE (1) | DE3786329T2 (fr) |
IL (1) | IL84455A (fr) |
IN (1) | IN169466B (fr) |
IT (1) | IT1199668B (fr) |
TR (1) | TR23950A (fr) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0300981A1 (fr) * | 1987-07-24 | 1989-01-25 | COBARR S.p.A. | Un procédé pour la réduction des impuretés dans les résines polyesters |
EP0334314A2 (fr) * | 1988-03-23 | 1989-09-27 | Mitsubishi Gas Chemical Company, Inc. | Méthode de préparation de résins polycarbonate purifiée |
EP0376119A2 (fr) * | 1988-12-27 | 1990-07-04 | COBARR S.p.A. | Procédé pour recycler des bouteilles de boisson en PET |
EP0419400A2 (fr) * | 1989-09-18 | 1991-03-27 | Shell Internationale Researchmaatschappij B.V. | Procédé pour la cristallisation de polynaphtalate d'éthylène |
WO1994001484A1 (fr) * | 1992-07-06 | 1994-01-20 | Buehler Ag | Procede de reduction de l'indice de jaune d'un granulat polyester postcondense |
US5656719A (en) * | 1995-02-20 | 1997-08-12 | Ems-Inventa Ag | Condensation injection molding process for producing bottle preforms of polyethylene terephthalate and/or its copolyesters and resultant preforms |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ZA964546B (en) * | 1995-06-06 | 1996-12-12 | Univ North Carolina | Process for the preparation of polyester in carbon dioxide |
US6288202B1 (en) | 1997-04-11 | 2001-09-11 | The University Of North Carolina At Chapel Hill | Synthesis of polycarbonates using Co2 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4161578A (en) * | 1978-05-12 | 1979-07-17 | Bepex Corporation | Process for solid phase polymerization of polyester |
DE3323940A1 (de) * | 1983-07-02 | 1985-01-10 | Hoechst Ag, 6230 Frankfurt | Verfahren zur reinigung von polymeren |
EP0227608A1 (fr) * | 1985-11-19 | 1987-07-01 | COBARR S.p.A. | Procédé de traitement d'articles creux, en particulier de préformes en téréphtalate de polyéthylène |
EP0300981A1 (fr) * | 1987-07-24 | 1989-01-25 | COBARR S.p.A. | Un procédé pour la réduction des impuretés dans les résines polyesters |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3544525A (en) * | 1968-03-26 | 1970-12-01 | Allied Chem | Process for crystallization,drying and solid-state polymerization of polyesters |
-
1986
- 1986-11-21 IT IT22424/86A patent/IT1199668B/it active
-
1987
- 1987-11-02 IN IN791/MAS/87A patent/IN169466B/en unknown
- 1987-11-12 AT AT87830402T patent/ATE90953T1/de not_active IP Right Cessation
- 1987-11-12 DE DE87830402T patent/DE3786329T2/de not_active Expired - Fee Related
- 1987-11-12 EP EP87830402A patent/EP0269583B1/fr not_active Expired - Lifetime
- 1987-11-12 IL IL84455A patent/IL84455A/xx not_active IP Right Cessation
- 1987-11-19 AT AT0305287A patent/AT398574B/de not_active IP Right Cessation
- 1987-12-20 TR TR87/0808A patent/TR23950A/xx unknown
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4161578A (en) * | 1978-05-12 | 1979-07-17 | Bepex Corporation | Process for solid phase polymerization of polyester |
DE3323940A1 (de) * | 1983-07-02 | 1985-01-10 | Hoechst Ag, 6230 Frankfurt | Verfahren zur reinigung von polymeren |
EP0227608A1 (fr) * | 1985-11-19 | 1987-07-01 | COBARR S.p.A. | Procédé de traitement d'articles creux, en particulier de préformes en téréphtalate de polyéthylène |
EP0300981A1 (fr) * | 1987-07-24 | 1989-01-25 | COBARR S.p.A. | Un procédé pour la réduction des impuretés dans les résines polyesters |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0300981A1 (fr) * | 1987-07-24 | 1989-01-25 | COBARR S.p.A. | Un procédé pour la réduction des impuretés dans les résines polyesters |
EP0334314A2 (fr) * | 1988-03-23 | 1989-09-27 | Mitsubishi Gas Chemical Company, Inc. | Méthode de préparation de résins polycarbonate purifiée |
EP0334314A3 (en) * | 1988-03-23 | 1990-07-25 | Mitsubishi Gas Chemical Company, Inc. | Method for producing purified polycarbonate resins |
EP0376119A2 (fr) * | 1988-12-27 | 1990-07-04 | COBARR S.p.A. | Procédé pour recycler des bouteilles de boisson en PET |
EP0376119A3 (fr) * | 1988-12-27 | 1991-01-09 | COBARR S.p.A. | Procédé pour recycler des bouteilles de boisson en PET |
EP0419400A2 (fr) * | 1989-09-18 | 1991-03-27 | Shell Internationale Researchmaatschappij B.V. | Procédé pour la cristallisation de polynaphtalate d'éthylène |
EP0419400A3 (en) * | 1989-09-18 | 1992-04-22 | The Goodyear Tire & Rubber Company | Process for crystallization of polyethylene naphthalate |
WO1994001484A1 (fr) * | 1992-07-06 | 1994-01-20 | Buehler Ag | Procede de reduction de l'indice de jaune d'un granulat polyester postcondense |
US5656719A (en) * | 1995-02-20 | 1997-08-12 | Ems-Inventa Ag | Condensation injection molding process for producing bottle preforms of polyethylene terephthalate and/or its copolyesters and resultant preforms |
Also Published As
Publication number | Publication date |
---|---|
IN169466B (fr) | 1991-10-19 |
AT398574B (de) | 1994-12-27 |
EP0269583B1 (fr) | 1993-06-23 |
EP0269583A3 (en) | 1990-01-31 |
ATA305287A (de) | 1994-05-15 |
IL84455A0 (en) | 1988-04-29 |
DE3786329D1 (de) | 1993-07-29 |
IT8622424A1 (it) | 1988-05-21 |
IT8622424A0 (it) | 1986-11-21 |
DE3786329T2 (de) | 1993-10-28 |
ATE90953T1 (de) | 1993-07-15 |
TR23950A (tr) | 1990-12-21 |
IT1199668B (it) | 1988-12-30 |
IL84455A (en) | 1991-07-18 |
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